ce965622-d4d5-419a-822e-b7c675b116ae Acrylonitrile ; Propylene, ammonia, air ; Propylene ammonia oxidation method ; greater than or equal to0.2 million t/a; NESPS2 丙烯腈 ; 丙烯、氨、空气 ; 丙烯氨氧化法 ; 大于等于20万吨/年 ; 全国第二次污染普查数据 the Technical of end-of-pipe management technology for pollution Exhaust gasis/，Its Technical efficiency of end-of-pipe management0 Reference Parameters Materials production Organic chemicals 12 2019 the Technical of end-of-pipe management technology for pollution Exhaust gasis/，Its Technical efficiency of end-of-pipe management0 该工业过程用于使用丙烷氨氧化法大规模生产丙烯腈。该过程的设计处理能力为每年20万吨或以上。这种丙烯腈可能用于各种塑料、丙烯酸纤维和其他合成材料的生产。 Unit process, single operation None 第二次全国污染源普查产排污核算系数手册（试用版）,二级代码26,四级代码2653文件，在完整版文件中第4111页 This dataset is derived from the Pollution Source Census Report and contains information on pollution emissions and related products. However, it does not include data on energy or chemical consumption, nor does it provide information on waste or co-product generation. When utilizing this dataset, please supplement the missing data based on actual conditions before use 该数据集来源于污染源普查报告，包含污染物排放及相关产品信息，但不包含能源或化学品消耗数据，也不提供废弃物或共生产物产生信息。在使用该数据集时，请根据实际情况补充缺失数据后再使用。 Inventory: The internal review was done by several iteration steps concerning raw data validation, raw data documentation, representativity, completeness and consistency of modelling with regard to ISO 14040 and 14044. 清单： 内部审查通过几个迭代步骤完成，涉及原始数据验证、原始数据记录、代表性、完整性、与 ISO 14040 和 14044 有关的建模的一致性。 Tiangong LCI Data Working Group 天工LCI数据工作小组 The data was created by the Office of the Second National Pollution Source Census of the Ministry of Ecology and Environment, and the data was organized by the TianGong Plan team for ILCD format 生态环境部第二次全国污染源普查工作办公室创建数据，天工计划团队常慧敏整理数据为ILCD格式 2024-04-15T22:10:40.479333+08:00 00.01.005 https://lcadata.tiangong.world/showProcess.xhtml?uuid=ce965622-d4d5-419a-822e-b7c675b116ae&version=01.00.000&stock=TianGong Tiangong LCI Data Working Group 天工LCI数据工作小组 false Free of charge for all users and uses phosphorus, total Output 0.0 0.0 Calculated the Technical of end-of-pipe management technology for pollution phosphorus, totalis/，Its Technical efficiency of end-of-pipe management0 污染物指标总磷的末端治理技术是/，其效率为0。原文件中描述污染物类别为废水，污染物指标为总磷，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为总磷 particles (PM2.5 - PM10) Output 0.005 0.005 Calculated the Technical of end-of-pipe management technology for pollution particles (PM2.5 - PM10)isBag filter，Its Technical efficiency of end-of-pipe management95 污染物指标颗粒物的末端治理技术是袋式除尘，其效率为95，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废气，污染物指标为颗粒物，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为颗粒物 particles (PM2.5 - PM10) Output 0.005 0.005 Calculated the Technical of end-of-pipe management technology for pollution particles (PM2.5 - PM10)isElectric-bag composite precipitator，Its Technical efficiency of end-of-pipe management95 污染物指标颗粒物的末端治理技术是电袋组合，其效率为95，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废气，污染物指标为颗粒物，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为颗粒物 cyanide Output 8e-06 8e-06 Calculated the Technical of end-of-pipe management technology for pollution cyanideisChemical treatment，Its Technical efficiency of end-of-pipe management92 污染物指标氰化物的末端治理技术是化学处理法，其效率为92，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废水，污染物指标为氰化物，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为氰化物 cyanide Output 1e-05 1e-05 Calculated the Technical of end-of-pipe management technology for pollution cyanideisPhysicochemical treatment + aerobic biological treatment，Its Technical efficiency of end-of-pipe management90 污染物指标氰化物的末端治理技术是物理化学法+好氧生物处理法，其效率为90，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废水，污染物指标为氰化物，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为氰化物 cyanide Output 1e-05 1e-05 Calculated the Technical of end-of-pipe management technology for pollution cyanideisPhysicochemical treatment + anaerobic biological treatment + aerobic biological treatment，Its Technical efficiency of end-of-pipe management90 污染物指标氰化物的末端治理技术是物理化学法+厌氧生物处理法+好氧生物处理法，其效率为90，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废水，污染物指标为氰化物，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为氰化物 particles (PM2.5 - PM10) Output 0.03 0.03 Calculated the Technical of end-of-pipe management technology for pollution particles (PM2.5 - PM10)isSpray tower/water shock bath，Its Technical efficiency of end-of-pipe management70 污染物指标颗粒物的末端治理技术是喷淋塔/冲击水浴，其效率为70，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废气，污染物指标为颗粒物，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为颗粒物 particles (PM2.5 - PM10) Output 0.04 0.04 Calculated the Technical of end-of-pipe management technology for pollution particles (PM2.5 - PM10)isVenturi，Its Technical efficiency of end-of-pipe management60 污染物指标颗粒物的末端治理技术是文丘里，其效率为60，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废气，污染物指标为颗粒物，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为颗粒物 particles (PM2.5 - PM10) Output 0.07 0.07 Calculated the Technical of end-of-pipe management technology for pollution particles (PM2.5 - PM10)isMulti-tube cyclone dust removal，Its Technical efficiency of end-of-pipe management30 污染物指标颗粒物的末端治理技术是多管旋风，其效率为30，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废气，污染物指标为颗粒物，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为颗粒物 volatile organic compound Output 0.55 0.55 Calculated the Technical of end-of-pipe management technology for pollution volatile organic compoundisRegenerative catalytic combustion method，Its Technical efficiency of end-of-pipe management50 污染物指标挥发性有机物的末端治理技术是蓄热式化燃烧法，其效率为50，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废气，污染物指标为挥发性有机物，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为挥发性有机物 volatile organic compound Output 0.55 0.55 Calculated the treatment technology for the pollution of volatile organic compounddidn't offered，Its Technical efficiency of end-of-pipe management50 污染物指标挥发性有机物的末端治理技术是化燃烧法，其效率为50，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废气，污染物指标为挥发性有机物，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为挥发性有机物 volatile organic compound Output 0.66 0.66 Calculated the Technical of end-of-pipe management technology for pollution volatile organic compoundisAdsorption + steam desorption，Its Technical efficiency of end-of-pipe management40 污染物指标挥发性有机物的末端治理技术是吸附+蒸气解析，其效率为40，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废气，污染物指标为挥发性有机物，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为挥发性有机物 acryolonitrile Output 1000.0 1000.0 Calculated nan 源文件中描述为为丙烯腈，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为工业废水量 Waste water Output 1690.0 1690.0 Calculated the Technical of end-of-pipe management technology for pollution Waste wateris/，Its Technical efficiency of end-of-pipe management0 污染物指标工业废水量的末端治理技术是/，其效率为0。原文件中描述污染物类别为废水，污染物指标为工业废水量，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为工业废水量 Petroleum-related waste Output 0.00215 0.00215 Calculated the Technical of end-of-pipe management technology for pollution Petroleum-related wasteisPhysicochemical treatment，Its Technical efficiency of end-of-pipe management90 污染物指标石油类的末端治理技术是物理化学处理法，其效率为90，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废水，污染物指标为石油类，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为石油类 Ammonia Nitrogen Output 0.00401 0.00401 Calculated the Technical of end-of-pipe management technology for pollution Ammonia NitrogenisChemical treatment，Its Technical efficiency of end-of-pipe management90 污染物指标氨氮的末端治理技术是化学处理法，其效率为90，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废水，污染物指标为氨氮，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为氨氮 Ammonia Nitrogen Output 0.00401 0.00401 Calculated the Technical of end-of-pipe management technology for pollution Ammonia NitrogenisPhysicochemical treatment + anaerobic biological treatment + activated sludge process，Its Technical efficiency of end-of-pipe management90 污染物指标氨氮的末端治理技术是物理化学法+厌氧生物处理法+活性污泥法，其效率为90，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废水，污染物指标为氨氮，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为氨氮 Ammonia Nitrogen Output 0.00401 0.00401 Calculated the Technical of end-of-pipe management technology for pollution Ammonia NitrogenisPhysicochemical treatment + anaerobic biological treatment + biofilm process，Its Technical efficiency of end-of-pipe management90 污染物指标氨氮的末端治理技术是物理化学法+厌氧生物处理法+生物膜法，其效率为90，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废水，污染物指标为氨氮，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为氨氮 Petroleum-related waste Output 0.00645 0.00645 Calculated the Technical of end-of-pipe management technology for pollution Petroleum-related wasteisPhysical treatment，Its Technical efficiency of end-of-pipe management70 污染物指标石油类的末端治理技术是物理处理法，其效率为70，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废水，污染物指标为石油类，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为石油类 Petroleum-related waste Output 0.0086 0.0086 Calculated the Technical of end-of-pipe management technology for pollution Petroleum-related wasteisChemical treatment，Its Technical efficiency of end-of-pipe management60 污染物指标石油类的末端治理技术是化学处理法，其效率为60，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废水，污染物指标为石油类，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为石油类 Nitrogen, organic bound Output 0.035 0.035 Calculated the Technical of end-of-pipe management technology for pollution Nitrogen, organic boundisPhysicochemical treatment + activated sludge process，Its Technical efficiency of end-of-pipe management90 污染物指标总氮的末端治理技术是物理化学法+活性污泥法，其效率为90，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废水，污染物指标为总氮，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为总氮 Nitrogen, organic bound Output 0.035 0.035 Calculated the Technical of end-of-pipe management technology for pollution Nitrogen, organic boundisPhysicochemical treatment + anaerobic biological treatment + activated sludge process，Its Technical efficiency of end-of-pipe management90 污染物指标总氮的末端治理技术是物理化学法+厌氧生物处理法+活性污泥法，其效率为90，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废水，污染物指标为总氮，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为总氮 Nitrogen, organic bound Output 0.035 0.035 Calculated the Technical of end-of-pipe management technology for pollution Nitrogen, organic boundisPhysicochemical treatment + anaerobic biological treatment + biofilm process，Its Technical efficiency of end-of-pipe management90 污染物指标总氮的末端治理技术是物理化学法+厌氧生物处理法+生物膜法，其效率为90，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废水，污染物指标为总氮，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为总氮 Nitrogen, organic bound Output 0.035 0.035 Calculated the Technical of end-of-pipe management technology for pollution Nitrogen, organic boundisPhysicochemical treatment + biofilm process，Its Technical efficiency of end-of-pipe management90 污染物指标总氮的末端治理技术是物理化学法+生物膜法，其效率为90，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废水，污染物指标为总氮，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为总氮 chemical oxygen demand Output 0.313 0.313 Calculated the Technical of end-of-pipe management technology for pollution chemical oxygen demandisPhysicochemical treatment + anaerobic biological treatment + activated sludge process，Its Technical efficiency of end-of-pipe management90 污染物指标化学需氧量的末端治理技术是物理化学法+厌氧生物处理法+活性污泥法，其效率为90，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废水，污染物指标为化学需氧量，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为化学需氧量 chemical oxygen demand Output 0.313 0.313 Calculated the Technical of end-of-pipe management technology for pollution chemical oxygen demandisPhysicochemical treatment + anaerobic biological treatment + biofilm process，Its Technical efficiency of end-of-pipe management90 污染物指标化学需氧量的末端治理技术是物理化学法+厌氧生物处理法+生物膜法，其效率为90，末端治理设施实际运行率（k值）计算公式为k=设施年耗电量（千瓦时/(设备功率(千瓦)×年运行小时数(时))。原文件中描述污染物类别为废水，污染物指标为化学需氧量，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为化学需氧量 Exhaust gas Output 6720.0 6720.0 Calculated the Technical of end-of-pipe management technology for pollution Exhaust gasis/，Its Technical efficiency of end-of-pipe management0 污染物指标工业废气量的末端治理技术是/，其效率为0。原文件中描述污染物类别为废气，污染物指标为工业废气量，此处对其进行了匹配工作，将其匹配到LCAflow库里面相最符合的流，污染物指标备注为工业废气量